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- W2376004032 abstract "Experiments were carried out in the ranges of 2-4 L/min CO2 flow rates,0.144-0.200mm feed particle sizes,33-48 ℃ temperatures and 10-25 MPa pressures.A mathematical model of the supercritical extraction process was developed on the basis of the differential mass balances performed along the extraction bed and the feed particle.Results show that the extraction curves were dependent of flow rate and feed particle size in a plot of oil yield versus extraction time.This indicated that the extraction process is influenced by both intraparticle diffusion and film mass transfer.In the case of temperature effect,a crossover effect was observed.The extraction rate increased as the pressure increased due to an increase in the solvent density.The results show that the CO2 flow rate,feed particle size,temperature and pressure affect the oil yield remarkably and that the mass transfer of the present system could be well described by the model employed herein." @default.
- W2376004032 created "2016-06-24" @default.
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- W2376004032 date "2010-01-01" @default.
- W2376004032 modified "2023-09-23" @default.
- W2376004032 title "Experimental Study and Simulation of Supercritical CO_2 Extraction for Essential Oil from Aucklandia Lappa Decne" @default.
- W2376004032 hasPublicationYear "2010" @default.
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